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dc.contributor.authorLoh, A
dc.contributor.authorLi, X
dc.contributor.authorSluijter, S
dc.contributor.authorShirvanian, P
dc.contributor.authorLai, Q
dc.contributor.authorLiang, Y
dc.date.accessioned2023-05-04T14:27:43Z
dc.date.issued2023-05-04
dc.date.updated2023-05-04T13:28:33Z
dc.description.abstractThe design of a 10 cm2 (3.4 cm by 3.4 cm) and a 100 cm2 (10 cm by 10 cm) anion exchange membrane (AEM) water electrolyser cell for hydrogen production are described. The AEM cells are based on a zero-gap configuration where the AEM is sandwiched between the anode and cathode so as to minimise voltage drop between the electrodes. Nonprecious nickel-based metal alloy and metal oxide catalysts were employed. Various experiments were carried out to understand the effects of operating parameters such as current densities, electrolyte concentrations, and testing regimes on the performance of both 10 cm2 and 100 cm2 AEM electrolyser cells. Increasing electrolyte concentration was seen to result in reductions in overpotentials which were proportional to current applied, whilst the use of catalysts improved performance consistently over the range of current densities tested. Extended galvanostatic and intermittent tests were demonstrated on both 10 cm2 and 100 cm2 cells, with higher voltage efficiencies achieved with the use of electrocatalysts. Stability tests in the 100 cm2 AEM electrolyser cell assembled with catalyst-coated electrodes demonstrated that the cell voltages remained stable at 2.03 V and 2.17 V during 72 h operation in 4 M KOH and 1 M KOH electrolyte, respectively, at a current density of 0.3 A cm−2 at 323 K. The inclusion of cycling load tests in testing protocols is emphasized for rational evaluation of cell performance as this was observed to speed up the rate of degradation mechanisms such as membrane degradation.en_GB
dc.description.sponsorshipEuropean Regional Development Fund (ERDF)en_GB
dc.description.sponsorshipRoyal Academy of Engineering (RAE)en_GB
dc.format.extent257-271
dc.identifier.citationVol. 4 (2), pp. 257-271en_GB
dc.identifier.doihttps://doi.org/10.3390/hydrogen4020018
dc.identifier.grantnumber2S03-019en_GB
dc.identifier.urihttp://hdl.handle.net/10871/133082
dc.identifierORCID: 0000-0003-4450-4617 (Li, Xiaohong)
dc.language.isoenen_GB
dc.publisherMDPIen_GB
dc.rights© 2023 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/)en_GB
dc.subjectanion exchange membraneen_GB
dc.subjectwater electrolysisen_GB
dc.subjectzero-gapen_GB
dc.subjectflow-field channelen_GB
dc.subjecthydrogen productionen_GB
dc.subjecttest protocolsen_GB
dc.titleDesign and Scale-Up of Zero-Gap AEM Water Electrolysers for Hydrogen Productionen_GB
dc.typeArticleen_GB
dc.date.available2023-05-04T14:27:43Z
dc.descriptionThis is the final version. Available on open access from MDPI via the DOI in this recorden_GB
dc.identifier.eissn2673-4141
dc.identifier.journalHydrogenen_GB
dc.relation.ispartofHydrogen MDPI, 4
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/en_GB
dcterms.dateAccepted2023-04-30
dcterms.dateSubmitted2023-04-12
rioxxterms.versionVoRen_GB
rioxxterms.licenseref.startdate2023-05-04
rioxxterms.typeJournal Article/Reviewen_GB
refterms.dateFCD2023-05-04T13:28:36Z
refterms.versionFCDAM
refterms.dateFOA2023-05-04T14:28:01Z
refterms.panelBen_GB
refterms.dateFirstOnline2023-05-04


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© 2023 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/)
Except where otherwise noted, this item's licence is described as © 2023 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/)